Journal of the American Chemical Society
Article
of the reaction temperature and time (without changes in the
composition of the reaction mixture) was systematically studied
and the main results are discussed in the following.
observed that the heating rate played an important role. Up to
the moment, all the experiments were performed placing the
In a first step, kinetic parameters (without temperature changes)
were evaluated (Table 1, SC1−SC4), showing the formation of α-
AEPF-14 compound as a pure phase when short reaction times
are used (1 h) (SC1). The increase of reaction time up to 2 and
then to 3 h (SC2 and SC3, respectively) gave rise to a mixture of
α-AEPF-14, AEPF-15, and AEPF-16 in which α-AEPF-14 was
the principal component. The proportion of this mixture changed
after 2 days of reaction, when AEPF-15 compound became the
principal component of the mixture (SC4).
In order to study the thermodynamic effects, a series of
reactions were also performed increasing the reaction temperature
up to 170 °C (Table 1, SC5−SC8). Thus, when short reaction
times are used (1 h), a mixture of α-AEPF-14 and AEPF-15 was
determined (SC5) (∼50% of each phase). An increase of the
reaction time up to 2 and then to 3 h (SC6 and SC7) led to a
crystalline mixture for which the main component was AEPF-15,
together with traces of AEPF-16. The same result was obtained
after increasing the time of reaction up to 2 days (SC8).
Taking into account the important role that both the
thermodynamic and the kinetic effects play, several experiments
were then performed at a higher temperature (180 °C) and
longer reaction times (1, 5, and 10 days) (Table 1, SC9−
SC11). Under these hydrothermal conditions, when the time of
reaction was 1 day, a mixture of AEPF-16 and a new phase
named AEPF-17 was obtained (∼50% of each) (SC9).
Increasing the reaction time up to 5 and 10 days (SC10 and
SC11), the contribution of AEPF-17 in the mixture increased.
However, it was not possible to obtain either of the two
compounds as pure phases.
At this point, the pH was also considered as an additional
variable. Thus, in the next step, the effect of the pH increasing
up to 7 by using a NaOH solution (0.1 M) was investigated
(Table 1, SC12−SC14). By comparison of the sample obtained
after 1 day of reaction at pH 7 (SC12) to that obtained at pH 6
(SC9), it could be concluded that a higher pH value favors the
formation of AEPF-16 instead of AEPF-17. Finally, at longer
time periods (5 and 10 days) (SC13-SC14), AEPF-16 was
successfully isolated.
Once the AEPF-16 compound was synthesized as a pure
phase, several experiments were carried out to establish the
reaction conditions under which AEPF-17 could be isolated.
With this propose, a series of hydrothermal reactions were
performed to evaluate the effect of a higher temperature (200 °C)
(Table 1, SC15−SC17). Thus, after 1 day of reaction, a mixture
of AEPF-16 (major component) and AEPF-17 was obtained
(SC15). When longer reaction times are used, AEPF-17
became the principal mixture component (SC16−SC17).
However, yet under these conditions it was not possible to
isolate AEPF-17.
Table 2. Explored Solvothermal Synthesis Conditions on the
System 1 Mg+2:1 phen:1 H2L
SC
T
(°C)
time
(days)
H2O:Me2CO
phase
heating
16
18
200
200
5
5
1:0
1:0
AEPF-16, AEPF-17
fast
β-AEPF-14,
amorphous
slow
19
20
21
22
23
24
200
200
200
200
200
200
5
5
5
5
5
5
20:1
5:1
2:1
1:1
1:5
0:1
AEPF-17
amorphous
β-AEPF-14
β-AEPF-14
liquid
slow
slow
slow
slow
slow
slow
liquid
autoclave reactors in a preheated oven at the desired
temperatures (fast heating, SC16). However, in this case,
certain hydrothermal conditions were chosen and the reaction
was then repeated by using a slow heating treatment (5 °C·min−1,
slow heating, SC18). Surprisingly, under this slow heating
condition, a new compound was determined (named β-AEPF-
14, which is a polymorph of α-AEPF-14), together with an
important amorphous contribution. Taking into account this
interesting result, an optimization of solvothermal conditions
was carried out by using slow heating treatments (T = 200 °C
and 5 days reaction time), systematically varying the polarity of
the reaction media (H2O:Me2CO volume ratio). The main
results are presented in Table 2.
Thus, a decrease in the polarity (H2O:Me2CO volume ratios =
2:1 and 1:1) led to the successful formation of β-AEPF-14
as a pure phase (SC21 and SC22). In addition, at higher
H2O:Me2CO volume ratio of 20:1, AEPF-17 was also
synthesized as a pure phase (SC19). Finally, when the mixture
is mainly or totally composed by Me2CO (SC23 and SC24,),
the solvothermal reactions resulted in the formation of liquids.
To summarize all the above-mentioned results, after
rationally optimizing the synthesis procedures: (i) Two
AEPF-14 polymorphs were obtained as pure crystalline phases
under hydrothermal conditions (α-phase, SC1) and solvother-
mal conditions (β-phase, SC21) varying the polarity media; (ii)
In addition, AEPF-16 compound was isolated by increasing the
pH (SC13). (iii) AEPF-17 (as it occurs for β-AEPF-14) is
obtained as a pure crystalline phase under solvothermal
conditions, using slow heating treatments (SC19). Schemes 1
and 2 summarize the synthesis optimization procedures carried
out under hydrothermal and solvothermal conditions, respec-
tively, to obtain each new magnesium phase.
Crystal Structure Description and Topological Ana-
lyses. Details of the single crystal X-ray diffraction data
collection, cell parameters, and crystal structure refinement for the
five compounds presented in this work are given in Tables S1−S5
(Supporting Information). The corresponding ORTEP represen-
tations for these crystal structures are shown in Figures S1−S5
(Supporting Information). A summary of the structural and
topological features for AEPF-14 (α- and β-), AEPF-15, AEPF-
16, and AEPF-17 are depicted in Figure 1. Details about the
topological simplifications carried out are shown in Figure 2.
AEPF-14 Polymorphs. The [Mg(H2O)4(phen)]L com-
pound (AEPF-14) presents two different polymorphs, named
α- and β-phases, which were isolated under hydro- and
Taking into account the unsuccessful efforts to purify the
AEPF-17 phase under high-temperature hydrothermal con-
ditions (200 °C), we then introduced changes in the polarity of
the reaction media. For that purpose, a mixture of acetone
(Me2CO) and water was chosen as solvent media, using
different volume ratios (Table 2). It is worth mentioning that,
although a wide variety of conditions were investigated during
this work (the studied variables were as follows: time,
temperature, and H2O:Me2CO volume ratio), at the beginning
all the experiments resulted in the formation of liquids.
Moreover, during the development of this investigation it was
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dx.doi.org/10.1021/ja210564a | J. Am. Chem. Soc. 2012, 134, 4762−4771